EP1796152B1 - Cmp polishing agent and method for polishing substrate - Google Patents
Cmp polishing agent and method for polishing substrate Download PDFInfo
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- EP1796152B1 EP1796152B1 EP05766424.5A EP05766424A EP1796152B1 EP 1796152 B1 EP1796152 B1 EP 1796152B1 EP 05766424 A EP05766424 A EP 05766424A EP 1796152 B1 EP1796152 B1 EP 1796152B1
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- Prior art keywords
- polishing
- acid
- polishing slurry
- water
- film
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01L—SEMICONDUCTOR DEVICES NOT COVERED BY CLASS H10
- H01L21/00—Processes or apparatus adapted for the manufacture or treatment of semiconductor or solid state devices or of parts thereof
- H01L21/02—Manufacture or treatment of semiconductor devices or of parts thereof
- H01L21/04—Manufacture or treatment of semiconductor devices or of parts thereof the devices having potential barriers, e.g. a PN junction, depletion layer or carrier concentration layer
- H01L21/18—Manufacture or treatment of semiconductor devices or of parts thereof the devices having potential barriers, e.g. a PN junction, depletion layer or carrier concentration layer the devices having semiconductor bodies comprising elements of Group IV of the Periodic Table or AIIIBV compounds with or without impurities, e.g. doping materials
- H01L21/30—Treatment of semiconductor bodies using processes or apparatus not provided for in groups H01L21/20 - H01L21/26
- H01L21/302—Treatment of semiconductor bodies using processes or apparatus not provided for in groups H01L21/20 - H01L21/26 to change their surface-physical characteristics or shape, e.g. etching, polishing, cutting
- H01L21/304—Mechanical treatment, e.g. grinding, polishing, cutting
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01L—SEMICONDUCTOR DEVICES NOT COVERED BY CLASS H10
- H01L21/00—Processes or apparatus adapted for the manufacture or treatment of semiconductor or solid state devices or of parts thereof
- H01L21/02—Manufacture or treatment of semiconductor devices or of parts thereof
- H01L21/04—Manufacture or treatment of semiconductor devices or of parts thereof the devices having potential barriers, e.g. a PN junction, depletion layer or carrier concentration layer
- H01L21/18—Manufacture or treatment of semiconductor devices or of parts thereof the devices having potential barriers, e.g. a PN junction, depletion layer or carrier concentration layer the devices having semiconductor bodies comprising elements of Group IV of the Periodic Table or AIIIBV compounds with or without impurities, e.g. doping materials
- H01L21/30—Treatment of semiconductor bodies using processes or apparatus not provided for in groups H01L21/20 - H01L21/26
- H01L21/31—Treatment of semiconductor bodies using processes or apparatus not provided for in groups H01L21/20 - H01L21/26 to form insulating layers thereon, e.g. for masking or by using photolithographic techniques; After treatment of these layers; Selection of materials for these layers
- H01L21/3105—After-treatment
- H01L21/31051—Planarisation of the insulating layers
- H01L21/31053—Planarisation of the insulating layers involving a dielectric removal step
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09G—POLISHING COMPOSITIONS; SKI WAXES
- C09G1/00—Polishing compositions
- C09G1/02—Polishing compositions containing abrasives or grinding agents
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K3/00—Materials not provided for elsewhere
- C09K3/14—Anti-slip materials; Abrasives
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K3/00—Materials not provided for elsewhere
- C09K3/14—Anti-slip materials; Abrasives
- C09K3/1454—Abrasive powders, suspensions and pastes for polishing
- C09K3/1463—Aqueous liquid suspensions
Definitions
- the present invention relates to a CMP polishing slurry for use in a substrate surface-smoothening step in production of semiconductor devices, in particular in steps of smoothening an interlayer dielectric and BPSG (silicon dioxide film doped with boron and phosphorus) film, forming a shallow trench isolation, and others, and a method of polishing a substrate by using the CMP polishing slurry.
- BPSG silicon dioxide film doped with boron and phosphorus
- CMP chemical mechanical polishing
- inorganic insulation film layers such as a silicon oxide insulation film are formed by methods such as plasma CVD and low-pressure CVD.
- Polishing slurries of fumed silica are commonly studied as a chemical mechanical polishing slurry for use in smoothening of the inorganic insulation film layer.
- the fumed silica polishing slurries are produced by grain growth, for example, by oxidative thermolysis of tetrachlorosilane and subsequent pH adjustment.
- such an polishing slurry still has a problem that the polishing speed is lower.
- Shallow trench isolation has been used for isolation of devices in an integrated circuit in the generation of a design rule of 0.25 ⁇ m or later.
- CMP is used for removal of excessive silicon oxide films formed on a substrate and a stopper film smaller in polishing speed is formed under the silicon oxide film for termination of polishing.
- silicon nitride is used for the stopper film, and the difference in polishing speed between the silicon oxide film and the stopper film is preferably greater.
- Conventional colloidal silica-based polishing slurries have a smaller polishing speed ratio between the silicon oxide film and the stopper film at approximately 3, and thus, did not have properties practically usable for shallow trench isolation.
- cerium oxide polishing slurries have been used as polishing slurries for glass surface such as of a photomask and lens.
- Cerium oxide particles are softer than silica or alumina particles, less likely to cause scratching on the polishing surface and thus, useful for finishing mirror-surface polishing.
- the particles also have an advantage that the polishing speed therewith is faster than that of silica polishing slurries.
- CMP polishing slurries for semiconductor processing, containing a high-purity cerium oxide abrasive have been used. Such methods are described, for example, in Japanese Patent Application Laid-Open No. 10-106994 .
- WO 2004/010487 A describes a method of polishing a silicon oxide film with a slurry comprising cerium oxide abrasive grains, water, a water-soluble organic polymer, said slurry having a pH of 3.5 to 6.
- the present invention provides a polishing slurry and a polishing method allowing polishing of a silicon oxide film or the like at high speed without polishing scratch and also allowing easy process management in the CMP technology of smoothening an interlayer dielectric film, BPSGfilm, and insulation film for shallow trench isolation.
- the present invention relates to (1) a CMP polishing slurry according to claim 1.
- the present invention relates to (2) a polishing method of substrate according to claim 8.
- the present invention provides a polishing slurry and a polishing method allowing polishing of a silicon oxide film or the like uniformly at high speed without polishing scratch and also allowing easy process management in the CMP technology of smoothening films such as an interlayer dielectric film, BPSG film, and insulation film for shallow trench isolation.
- cerium oxide is obtained by oxidation of a cerium compound such as carbonate salt, nitrate salt, sulfate salt, or oxalate salt.
- a cerium oxide polishing slurry for use in polishing a silicon oxide film formed by TEOS CVD or other method allows higher-speed polishing, but causes more polishing scratches, when the crystal diameter of the particle becomes greater and the crystal distortion is smaller, i. e. , when the crystallinity thereof is higher.
- the method of producing cerium oxide particles for use in the present invention is not particularly limited, the crystal diameter of the cerium oxide is preferably 5 nm or more and 300 nm or less.
- the content of alkali metals and halogens is preferably reduced to 10 ppm or less in the cerium oxide particle because the particle is used for polishing during production of semiconductor devices.
- cerium oxide powder can be prepared, for example, by calcination, oxidation with hydrogen peroxide, or the like.
- the calcining temperature is preferably 350°C or higher and 900°C or lower.
- the cerium oxide particles prepared by the method are aggregate, and thus, preferably pulverized mechanically.
- the pulverization method is preferably a dry pulverization method, for example by using a jet mill, or a wet pulverization method, for example by using a planetary bead mill.
- the jet mill is described, for example, in Kagaku Kogaku Ronbunshu (Chemical Industrial Paper Collection), vol. 6, No. 5 (1980) pp. 527 to 532 .
- a method of dispersing such cerium oxide particles in water that is a main disperse medium includes, for example, a method of using homogenizer, ultrasonic dispersing machine, or wet process ball mill, aside from a method of dispersion process by using an ordinary agitator.
- microparticulating the cerium oxide dispersed by the above method is prepared by a sedimentation classification method of leaving the cerium oxide dispersion for a long period allowing sedimentation of larger particles and withdrawing the supernatant liquid by a pump.
- a high pressure homogenizer may be used for collision of the cerium oxide particles in the disperse medium mutually at high pressure.
- the average particle diameter of the cerium oxide particle thus prepared in the CMP polishing slurry is preferably 1 to 400 nm, more preferably 1 to 300 nm, and still more preferably 1 to 200 nm.
- An average particle diameter of cerium oxide particles of less than 1 nm may lead to decrease in polishing speed, while an average particle diameter of more than 400 nm may lead to more frequent scratching on the polished film.
- the average particle diameter of cerium oxide particles is the D50 value (median diameter of volumetric distribution, cumulative median value), as measured in a laser-diffraction particle size distribution analyzer.
- the CMP polishing slurry according to the present invention is prepared, for example, by blending the cerium oxide particles having the properties above, a dispersant and water to disperse the particles and adding a water-soluble polymer additionally.
- the concentration of the cerium oxide particles is preferably in the range of 0.1 weight part or more and 5 weight parts or less, more preferably 0.2 weight part or more and 2 weight parts or less, and still more preferably 0.5 weight part or more and 1.5 weight parts or less, with respect to 100 weight parts of the CMP polishing slurry.
- An excessively lower concentration leads to decrease in polishing speed, while an excessively higher concentration leads to aggregation.
- dispersants for use examples include water-soluble anionic dispersants, water-soluble nonionic dispersants, water-soluble cationic dispersants, water-soluble amphoteric dispersants, and the like.
- Polymer dispersants containing an ammonium acrylate salt as the copolymerization component are also favorable. Examples thereof include ammonium polyacrylate, copolymers of acrylic amide and ammonium acrylate, and the like.
- Two or more dispersants containing at least one polymer dispersant containing an ammonium acrylate salt as the copolymerization component and at least one dispersant selected from water-soluble anionic, nonionic, cationic, and amphoteric dispersants, may be used in combination. Because the dispersant is used in abrasion during production of semiconductor devices, the content of alkali metals such as sodium and potassium ions, halogen atoms and a sulfur atom in the dispersant is preferably reduced to 10 ppm or less.
- water-soluble anionic dispersants examples include triethanolamine laurylsulfate, ammonium laurylsulfate, triethanolamine polyoxyethylene alkylether sulfate, special polycarboxylate polymer dispersants, and the like.
- water-soluble nonionic dispersants examples include polyoxyethylene laurylether, polyoxyethylene cetylether, polyoxyethylene stearylether, polyoxyethylene oleylether, polyoxyethylene higher-alcohol ether, polyoxyethylene octylphenylether, polyoxyethylene nonylphenylether, polyoxyalkylene alkylether, polyoxyethylene derivatives, polyoxyethylene sorbitan monolaurate, polyoxyethylene sorbitan monopalmitate, polyoxyethylene sorbitan-monostearate, polyoxyethylene sorbitan tristearate, polyoxyethylene sorbitan monooleate, polyoxyethylene sorbitan trioleate, polyoxyethylene sorbitol tetraoleate, polyethylene glycol monolaurate, polyethylene glycol monostearate, polyethylene glycol distearate, polyethylene glycol monooleate, polyoxyethylene alkylamine, polyoxyethylene hydrogenated castor oil, 2-hydroxyethyl methacrylate, alkyl alkan
- water-soluble cationic dispersants examples include polyvinylpyrrolidone, coconut amine acetate, stearylamine acetate, and the like.
- water-soluble amphoteric dispersants examples include lauryl betaine, stearyl betaine, lauryldimethylamine oxide, 2-alkyl-N-carboxymethyl-N-hydroxyethylimidazoliniumbetaine, and the like.
- the amount of these dispersants added is preferably in the range of 0.01 weight part or more and 10 weight parts or less with respect to 100 weight parts of the cerium oxide particles, for improvement of dispersion and prevention of sedimentation of the particles in the polishing slurry and for a relation of polishing scratch and the amount of the dispersants.
- the molecular weight of the dispersant is preferably 100 to 50,000, more preferably 1,000 to 10,000.
- a dispersant having a molecular weight of less than 100 may cause decrease in the polishing speed when a silicon oxide or nitride film is polished, while a dispersant having a molecular weight of more than 50,000 may lead to increase in viscosity and deterioration in the storage stability of the CMP polishing slurry.
- the water-soluble polymer according to the present invention is a polymer obtained by radical polymerization of at least one monomer of a carboxylic acid having an unsaturated double bond and the salt thereof by using at least one of a cationic azo compound and the salt thereof as a polymerization initiator, and the polymer may be a copolymer.
- the carboxylic acids having an unsaturated double bond according to the present invention include acrylic acid, methacrylic acid, crotonic acid, vinylacetic acid, tiglic acid, 2-trifluoromethylacrylic acid, itaconic acid, fumaric acid, maleic acid, citraconic acid, mesaconic acid, gluconic acid, and the like, and these carboxylic acids may be used in combination of two or more.
- the salts of the carboxylic acid include ammonium, potassium, and alkylamine salts.
- the polymer may be a copolymer of the carboxylic acid and/or the salt thereof with a radical polymerizable monomer such as C 1 to C 18 acrylic ester, C 1 to C 18 methacrylic ester, acrylamide, vinylalcohol, acrylonitrile, vinylpyrrolidone, or vinylpyridine.
- a radical polymerizable monomer such as C 1 to C 18 acrylic ester, C 1 to C 18 methacrylic ester, acrylamide, vinylalcohol, acrylonitrile, vinylpyrrolidone, or vinylpyridine.
- Examples of the cationic azo compounds according to the present invention and the salts thereof include 2,2'-azobis[2-(5-methyl-2-imidazolin-2-yl)propane] hydrochloride, 2,2'-azobis[2-(2-imidazolin-2-yl)propane], 2,2'-azobis[(2-(2-imidazolin-2-yl)propane] hydrochloride, 2,2'-azobis[2-(2-imidazolin-2-yl)propane] sulfate hydrate, 2,2'-azobis[2-(3,4,5,6-tetrahydropyrimidin-2-yl)propane] hydrochloride, 2,2'-azobis ⁇ 2-[1-(2-hydroxyethyl)-2-imidazolin-2-yl]propane ⁇ hydrochloride, 2,2-azobis(2-amidino propane) hydrochloride, 2,2'-azobis(2-methylpropionamidoxime), and the like.
- These compounds may be used in combination of two or more, and organic salts thereof such as acetate, oxalate, malonate, succinate, malate, tartarate, and citrate and inorganic salts such as phosphate, hydrobromide, hydroiodide, and hydrofluoride are also usable.
- organic salts thereof such as acetate, oxalate, malonate, succinate, malate, tartarate, and citrate
- inorganic salts such as phosphate, hydrobromide, hydroiodide, and hydrofluoride are also usable.
- the solvent used during polymerization is not particularly limited, but, water or C 1 to C 4 alcohols such as methanol, isopropanol, propanol, and butanol are preferable, and these solvents may be used in combination.
- the weight-average molecular weight of the water-soluble polymer thus obtained is preferably in the range of 200 or more and 50,000 or less, more preferably 300 or more and 20,000 or less, and most preferably 500 or more and 10,000 or less.
- a molecular weight of less than 200 may lead to insufficient smoothening efficiency, while a molecular weight of more than 50,000 may lead to aggregation of cerium oxide particles.
- a mercapto compound-based molecular weight adjustor such as mercaptoethanol may be used.
- the blending amount of the water-soluble polymer according to the present invention is preferably in the range of 0.01 weight part or more and 5 weight parts or less, more preferably 0.05 weight part or more and 3 weight parts or less, and most preferably 0.1 weight part or more and 1 weight part or less, with respect to 100 weight parts of the CMP polishing slurry.
- An excessively smaller addition amount leads to decrease in smoothening efficiency, while an excessively large amount leads to aggregation of cerium oxide particles.
- the polishing slurry according to the present invention may contain another water-soluble polymer.
- the another water-soluble polymer is not particularly limited, and examples thereof include polysaccharides such as alginic acid, pectin acid, carboxymethylcellulose, agar, curdlan and pullulan; polycarboxylic acids such as polyaspartic acid, polyglutamic acid, polylysine, polymalic acid, polyamide acid, polyamide acid ammonium salt, polyamide acid sodium salt and polyglyoxylic acid and the salt thereof; and vinyl polymers such as polyvinylalcohol, polyvinylpyrrolidone and polyacrolein.
- the weight-average molecular weight of the water-soluble polymer is preferably 500 or more, and the blending amount thereof is preferably in the range of 0.01 weight part or more and 5 weight parts or less with respect to 100 weight parts of the CMP polishing slurry.
- the polishing slurry according to the present invention shows stabilized properties even when it is stored as a two-liquid CMP polishing slurry composed of a cerium oxide slurry containing cerium oxide particles, a dispersant and water and an additional solution containing a water-soluble polymer and water, and also even when it is stored as a polishing slurry previously containing the water-soluble polymer.
- the polishing slurry is stored as the two-liquid polishing slurry composed of a cerium oxide slurry and an additional solution, it is possible to adjust the smoothening efficiency and the polishing speed easily by changing the blending ratio of these two liquids.
- the additional solution and the cerium oxide slurry are fed to a polishing table as they are supplied separately from different pipes and mixed immediately before a supply pipe outlet where these pipes are connected, or the additional solution is mixed with the cerium oxide slurry immediately before polishing.
- the CMP polishing slurry according to the present invention is used for polishing after it is adjusted to a desirable pH.
- a pH adjuster for use is not particularly limited, but ammonia water or an acid component is used more favorably than alkali metals when the polishing slurry is used for semiconductor polishing.
- the pH may be adjusted with the ammonium salt of the water-soluble polymer previously partially neutralized with ammonia.
- the pH of the CMP polishing slurry is according to the invention 4.5 or more and 6.0 or less, more preferably 4.8 or more and 5 . 6 or less. An excessively low pH leads to decrease in polishing speed, while an excessively high pH leads to deterioration in smoothness.
- the pH of the CMP polishing slurry according to the present invention was measured by using a pH meter (for example, Model PH81, manufactured by Yokogawa Electric Corporation). After two-point calibration with a standard buffer solution (phthalate buffer solution, pH: 4.21 (25°C) and a neutral phosphate buffer solution, pH: 6.86 (25°C)), an electrode was immersed in the CMP polishing slurry, and the pH stabilized after 2 minutes or more was measured.
- a pH meter for example, Model PH81, manufactured by Yokogawa Electric Corporation.
- the polishing method according to the present invention is characterized by polishing a film to be polished by pressing a substrate having the film to be polished against a polishing cloth of a polishing table and moving the substrate and the polishing tablerelatively to each other while supplying the CMP polishing slurry according to the present invention to the space between the film to be polished and the polishing cloth, wherein the film to be polished is an inorganic insulation layer formed on a semiconductor substrate.
- the substrates include substrates for semiconductor device production, for example, substrates having an inorganic insulation layer formed on a semiconductor substrate such as a semiconductor substrate having a circuit element and a wiring pattern formed thereon and a semiconductor substrate having a circuit element formed thereon.
- the films to be polished include the inorganic insulation layers described above including a silicon oxide film layer, silicon nitride and silicon oxide film layers, and the like. Surface irregularity of the silicon oxide film layer is eliminated by polishing the silicon oxide or nitride film layer formed on the semiconductor substrate with the CMP polishing slurry above, and the semiconductor substrate is smoothened over the entire surface.
- the substrate can also be used for shallow trench isolation.
- the ratio of the silicon-oxide-film polishing speed to the silicon-nitride-film polishing speed is preferably 10 or more.
- the difference between the silicon-oxide-f ilmpolishing speed and the silicon nitride film polishing speed is small at a ratio of less than 10, and it is difficult to stop abrasion at a predetermined position during shallow trench isolation.
- the polishing speed of the silicon nitride film becomes far smaller at a ratio of 10 or more, and thus, it is possible to stop abrasion easily and thus such a high ratio is more favorable for shallow trench isolation.
- the substrate is preferably protected from scratching during polishing for use in shallow trench isolation.
- polishing method will be described, by taking a semiconductor substrate having an inorganic insulation layer formed thereon as an example.
- a general polishing machine having a holder holding a substrate formed a film to be polished such as a semiconductor substrate and having a polishing table allowing attachment of a polishing cloth (pad) equipped with a rotational frequency-adjustable motor or the like may be used as the polishing machine.
- a polishing machine EPO-111, manufactured by Ebara Corporation may be used.
- the polishing cloth may be common nonwoven fabric, expanded polyurethane, porous fluoroplastic, or the like, but is not particularly limited.
- the polishing cloth is preferably processed to have grooves for holding the CMP polishing slurry.
- the polishing condition is not particularly limited, but the rotational velocity of the polishing table is preferably lower at 200 rpm or less for prevention of separation of the semiconductor substrate, and the pressure applied to the semiconductor substrate (processing load) is preferably not larger than 100 kPa for prevention of scratching after polishing.
- a CMP polishing slurry is supplied continuously onto the polishing cloth, for example, by a pump during polishing.
- the feed rate is not particularly limited, but the surface of the polishing cloth is preferably covered with the CMP polishing slurry all the time.
- the semiconductor substrate after polishing is preferably washed thoroughly with running water and dried while the water droplets remaining on the semiconductor substrate are removed, for example, with a spin drier. It is possible to eliminate surface irregularity and to make the semiconductor substrate smoothened over the entire surface by polishing the film, an inorganic insulation layer, to be polished with the polishing slurry. After the smoothened shallow trench is formed, aluminum wiring is formed on the silicon oxide insulation film layer; a silicon oxide insulation film is formed between and on the wirings by the method above; and the film is then surface-smoothened similarly by polishing with the CMP polishing slurry. It is possible to produce a semiconductor substrate having a desired number of layers by repeating the step several times.
- convex regions thereon should be polished selectively.
- a protection film is formed on the surface of the cerium oxide particles and the film to be polished.
- the water-soluble polymer according to the present invention which has a polymerization initiator cationic azo compound bound to its terminal, is adsorbed electrostatically on the negatively-charged silicon oxide film in the weakly acidic to neutral range. As a result, a protection film is formed on the surface of the film to be polished uniformly and efficiently, and the wafer surface is polished uniformly.
- the inorganic insulation film to which the CMP polishing slurry according to the invention is used is produced, for example, by low-pressure CVD, plasma CVD, or the like.
- monosilane SiH 4 is used as a Si source and oxygen O 2 is used as an oxygen source .
- the film is obtained in the SiH 4 -O 2 oxidation reaction at a temperature of 400°C or lower.
- the film is heat-treated as needed after CVD at a temperature of 1, 000°C or lower.
- phosphorus P is doped for surface smoothening by high temperature reflow, use of a SiH 4 -O 2 -PH 3 reaction gas is preferable .
- the plasma CVD method has an advantage that the chemical reaction, which demands high temperature under normal thermal equilibrium, can be carried out at low temperature.
- the plasma generation methods include two methods: a capacitively coupled method and an inductively coupled method.
- the reaction gases include SiH 4 -N 2 O gas containing SiH 4 as the Si source and N 2 O as the oxygen source; and a TEOS-O gas (TEOS-plasma CVD method) containing tetraethoxysilane (TEOS) as the Si source.
- the substrate temperature is preferably 250°C to 400°C, and the reaction pressure is preferably in the range of 67 to 400 Pa.
- the silicon oxide film according to the present invention may be doped with an element such as phosphorus or boron.
- the silicon nitride film is formed by low-pressure CVD at a high temperature of 900°C in the SiH 2 Cl 2 -NH 3 oxidation reaction, while dichlorosilane SiH 2 Cl 2 is used as the Si source and ammonia NH 3 as the nitrogen source.
- the reaction gas used in the plasma CVD method is a SiH 4 -NH 3 gas containing SiH 4 as the Si source and NH 3 as the nitrogen source.
- the substrate temperature is preferably 300°C to 400°C.
- the CMP polishing slurry and the polishing method according to the present invention can be applied not only to the silicon oxide film formed on a semiconductor substrate but also in the production processes for various semiconductor devices.
- they may be used for polishing of silicon oxide films formed on a wiring board having a predetermined wiring; inorganic insulation films of glass, silicon nitride or the like; films mainly containing polysilicon, Al, Cu, Ti, TiN, W, Ta, TaN, or the like; optical glasses such as photomask, lens, and prism; inorganic conductive films such as ITO; optical integrated circuit, photoswitching element, optical waveguides made of glass or a crystalline material; an end face of an optical fiber; optical single crystals such as scintillator; solid-state laser single crystals; blue laser LED sapphire substrates; semiconductor single crystals such as SiC, GaP, and GaAs; , glass plates for magnetic disk; magnetism heads, and the like.
- the weight-average molecular weight of the polyacrylic acid thus obtained was 5,000 (as polyethylene glycol).
- the supernatant cerium oxide dispersion obtained was diluted with deionized water to a solid matter concentration of 5 weight%, to give a cerium oxide slurry.
- the slurry was diluted to a suitable concentration for measurement of the average particle diameter of the particles in the cerium oxide slurry, and the average particle diameter D50, as measured by using a laser-diffraction particle size distribution analyzer Master Sizer Microplus (trade name, manufactured by Malvern) at a refractive index of 1.93 and an absorption of 0, was 170 nm.
- the amount of impurity ions Na, K, Fe, Al, Zr, Cu, Si, and Ti
- a 864 wafer manufactured by SEMATECH ( ⁇ 200 mm, SiN film thickness: 150 nm, SiO 2 film thickness: 610 nm in convex region and 610 nm in concave region) was used as a test wafer for evaluation of shallow-trench-isolation (STI) insulation film CMP.
- the test wafer was attached to a holder of a polishing machine (trade name: Mirra, manufactured by Applied Materials) having an adsorption pad for fixing a substrate to be held, while a porous urethane resin polishing pad IC-1000 (K groove) manufactured by Rodel was connected to a polishing table of ⁇ 480 mm.
- the holder was placed on the pad with its insulation film face facing downward, and the pressures of membrane, retainer ring, and inner tube were respectively set to 3.0 psi, 3.5 psi, and 3.0 psi (20.6 Pa, 24.0 Pa, and 20.6 Pa) as the processing load.
- the test wafer for evaluation of the STI insulation film CMP was polished while the polishing table and the wafer were moved respectively to each other at a speed of 98 rpm and 78 rpm and the CMP polishing slurry thus prepared was fed onto the polishing table dropwise at a rate of 200 milliliter/minute.
- the end point of polishing was determined by monitoring a torque current value of the polishing table.
- the wafer after polishing was washed thoroughly with purified water and then dried.
- the thickness of the residual insulation film in the concave and convex regions, or the residual SiN film was measured by using an optical interference thickness meter (trade name: Nanospec AFT-5100, manufactured by Nanometrics Inc.).
- the difference in level between the convex region and the concave region after polishing was measured by using a level difference meter Dektak V200-Si manufactured by Veeco. The results are summarized in Table 1.
- aqueous polyacrylate solution thus obtained (25 weight%) and 2, 352 g of deionized water were mixed, and the mixture was adjusted to pH 5.3 with ammonia water (25 weight%). Additionally, 600 g of the cerium oxide slurry (solid matter: 5 weight%) was added thereto, to give a cerium oxide-based CMP polishing slurry (solid matter: 1.0 weight%).
- the polishing slurry had a pH of 5.5, and the average particle diameter of the particles in the polishing slurry, as measured by a laser-diffraction particle size distribution analyzer after dilution to a suitable concentration, was 170 nm.
- a test wafer for evaluation of shallow-trench-isolation (STI) insulation film CMP was polished in the same manner as in Example 1, except that the polishing slurry thus prepared was used. The results are summarized in Table 1.
- a test wafer for evaluation of shallow-trench-isolation (STI) insulation film CMP was polished in the same manner as in Example 1, except that the polishing slurry thus prepared was used. The results are summarized in Table 1.
- aqueous polyacrylic acid-methacrylic acid copolymer solution obtained above 25 weight% was mixed with 2,370 g of deionized water, and the mixture was adjusted to pH 4.6 with ammonia water (25 weight%). Additionally, 600 g of the cerium oxide slurry (solid matter: 5 weight%) was added thereto, to give a cerium oxide-based CMP polishing slurry (solid matter: 1.0 weight%) .
- the polishing slurry had a pH of 4.8, and the average particle diameter of the particles in the polishing slurry, as measured by a laser-diffraction particle size distribution analyzer after dilution to a suitable concentration, was 170 nm.
- a test wafer for evaluation of shallow-trench-isolation (STI) insulation film CMP was polished in the same manner as in Example 1, except that the polishing slurry thus prepared was used. The results are summarized in Table 1.
- aqueous polyacrylate solution 25 weight% and 2,370 g of deionized water were mixed, and the mixture was adjusted to pH 6.9 with ammonia water (25 weight%). Additionally, 600 g of the cerium oxide slurry (solid matter: 5 weight%) was added thereto, to give a cerium oxide polishing slurry (solid matter: 1.0 weight%).
- the polishing slurry had a pH of 7.0, and the average particle diameter of the particles in the polishing slurry, as measured by using a laser-diffraction particle size distribution analyzer after dilution to a suitable concentration, was 170 nm.
- Example 1 A test wafer for evaluation of shallow-trench-isolation (STI) insulation film CMP was polished in the same manner as in Example 1, except that the polishing slurry obtained was used. As a result, a period as long as 300 seconds was needed for exposure of the SiN film in the high-density area (convex region: 100%), indicating that the polishing speed is lower. On the other hand, the SiN film in the low-density area (convex region: 10%) was also polished completely, indicating the polishing proceeded unevenly according to the pattern density.
- STI shallow-trench-isolation
- the present invention provides a polishing slurry and a polishing method allowing polishing of a silicon oxide film or the like without polishing scratch uniformly at high speed and also allowing easy process management in the CMP technology of smoothening films such as an interlayer dielectric film, BPSG film, and insulation film for shallow trench isolation.
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- Physics & Mathematics (AREA)
- Power Engineering (AREA)
- General Physics & Mathematics (AREA)
- Materials Engineering (AREA)
- Condensed Matter Physics & Semiconductors (AREA)
- Mechanical Treatment Of Semiconductor (AREA)
- Finish Polishing, Edge Sharpening, And Grinding By Specific Grinding Devices (AREA)
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2004216039 | 2004-07-23 | ||
| PCT/JP2005/013283 WO2006009160A1 (ja) | 2004-07-23 | 2005-07-20 | Cmp研磨剤及び基板の研磨方法 |
Publications (3)
| Publication Number | Publication Date |
|---|---|
| EP1796152A1 EP1796152A1 (en) | 2007-06-13 |
| EP1796152A4 EP1796152A4 (en) | 2008-12-03 |
| EP1796152B1 true EP1796152B1 (en) | 2019-02-27 |
Family
ID=35785268
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP05766424.5A Expired - Lifetime EP1796152B1 (en) | 2004-07-23 | 2005-07-20 | Cmp polishing agent and method for polishing substrate |
Country Status (7)
| Country | Link |
|---|---|
| US (1) | US9293344B2 (enExample) |
| EP (1) | EP1796152B1 (enExample) |
| JP (3) | JPWO2006009160A1 (enExample) |
| KR (1) | KR100856171B1 (enExample) |
| CN (3) | CN1985361A (enExample) |
| TW (1) | TWI287040B (enExample) |
| WO (1) | WO2006009160A1 (enExample) |
Families Citing this family (20)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101126124B1 (ko) * | 2005-05-30 | 2012-03-30 | 주식회사 동진쎄미켐 | 연마 평탄도를 향상시킨 산화 세륨 슬러리 조성물 |
| CN101375376B (zh) | 2006-01-31 | 2012-09-19 | 日立化成工业株式会社 | 绝缘膜研磨用cmp研磨剂、研磨方法、通过该研磨方法研磨的半导体电子部件 |
| MD3809C2 (ro) * | 2008-06-26 | 2009-08-31 | Акционерное Общество "Azurit" | Procedeu de prelucrare de finisare a plăcilor pentru acoperire din calcar hemogen |
| JP5632378B2 (ja) * | 2008-09-26 | 2014-11-26 | ロディア オペレーションズRhodia Operations | 化学機械研磨用研磨剤組成物及びその使用法 |
| DE112012004431T5 (de) * | 2011-10-24 | 2014-07-10 | Fujimi Incorporated | Zusammensetzung zu Polierzwecken, Polierverfahren unter Verwendung derselben und Verfahren zur Herstellung eines Substrates |
| US8703004B2 (en) * | 2011-11-14 | 2014-04-22 | Kabushiki Kaisha Toshiba | Method for chemical planarization and chemical planarization apparatus |
| US9299573B2 (en) | 2012-03-14 | 2016-03-29 | Hitachi Chemical Company, Ltd. | Polishing method |
| EP2826827B1 (en) * | 2013-07-18 | 2019-06-12 | Basf Se | CMP composition comprising abrasive particles containing ceria |
| JP2016175948A (ja) * | 2013-08-09 | 2016-10-06 | コニカミノルタ株式会社 | Cmp用研磨液 |
| WO2015046163A1 (ja) * | 2013-09-30 | 2015-04-02 | 株式会社フジミインコーポレーテッド | 研磨用組成物およびその製造方法 |
| JP5920840B2 (ja) * | 2013-09-30 | 2016-05-18 | 株式会社フジミインコーポレーテッド | 研磨用組成物およびその製造方法 |
| CN104356950B (zh) * | 2014-10-21 | 2017-01-18 | 李金平 | 一种蓝宝石晶片抛光液 |
| JP6206388B2 (ja) * | 2014-12-15 | 2017-10-04 | 信越半導体株式会社 | シリコンウェーハの研磨方法 |
| CN104987839A (zh) * | 2015-06-30 | 2015-10-21 | 安徽德诺化工有限公司 | Led用蓝宝石衬底研磨液 |
| CN110998800B (zh) * | 2017-08-14 | 2023-09-22 | 株式会社力森诺科 | 研磨液、研磨液套剂及研磨方法 |
| WO2019064524A1 (ja) | 2017-09-29 | 2019-04-04 | 日立化成株式会社 | 研磨液、研磨液セット及び研磨方法 |
| JP6837958B2 (ja) | 2017-12-28 | 2021-03-03 | 花王株式会社 | 酸化珪素膜用研磨液組成物 |
| US11718767B2 (en) | 2018-08-09 | 2023-08-08 | Versum Materials Us, Llc | Chemical mechanical planarization composition for polishing oxide materials and method of use thereof |
| JP7216880B2 (ja) | 2019-02-19 | 2023-02-02 | 株式会社レゾナック | 研磨液及び研磨方法 |
| CN111014695A (zh) * | 2019-11-21 | 2020-04-17 | 苏州新锐合金工具股份有限公司 | 硬质合金混合料的制备方法 |
Family Cites Families (35)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0661302B1 (en) | 1993-12-23 | 1999-09-01 | Nitto Denko Corporation | Process for producing aqueous Dispersion-Type Acrylic Polymer, the acrylic polymer obtained thereby, and pressure-sensitive adhesive comprising the acrylic polymer |
| JP3278532B2 (ja) | 1994-07-08 | 2002-04-30 | 株式会社東芝 | 半導体装置の製造方法 |
| JPH10106994A (ja) | 1997-01-28 | 1998-04-24 | Hitachi Chem Co Ltd | 酸化セリウム研磨剤及び基板の研磨法 |
| JP3915042B2 (ja) | 1997-02-18 | 2007-05-16 | 三井化学株式会社 | 研磨材及び研磨方法 |
| WO2000039843A1 (en) | 1998-12-25 | 2000-07-06 | Hitachi Chemical Company, Ltd. | Cmp abrasive, liquid additive for cmp abrasive and method for polishing substrate |
| KR100472882B1 (ko) | 1999-01-18 | 2005-03-07 | 가부시끼가이샤 도시바 | 수계 분산체, 이를 이용한 화학 기계 연마용 수계 분산체조성물, 웨이퍼 표면의 연마 방법 및 반도체 장치의 제조방법 |
| KR100447551B1 (ko) | 1999-01-18 | 2004-09-08 | 가부시끼가이샤 도시바 | 복합 입자 및 그의 제조 방법, 수계 분산체, 화학 기계연마용 수계 분산체 조성물 및 반도체 장치의 제조 방법 |
| JP4406111B2 (ja) * | 1999-04-28 | 2010-01-27 | 花王株式会社 | 研磨液組成物 |
| JP3912927B2 (ja) | 1999-05-10 | 2007-05-09 | 花王株式会社 | 研磨液組成物 |
| JP2001007059A (ja) | 1999-06-18 | 2001-01-12 | Hitachi Chem Co Ltd | Cmp研磨剤及び基板の研磨方法 |
| JP2001007061A (ja) | 1999-06-18 | 2001-01-12 | Hitachi Chem Co Ltd | Cmp研磨剤及び基板の研磨方法 |
| JP4224659B2 (ja) | 1999-06-23 | 2009-02-18 | Jsr株式会社 | 半導体部品用洗浄剤 |
| JP4134458B2 (ja) | 1999-06-23 | 2008-08-20 | Jsr株式会社 | 半導体部品用洗浄剤、半導体部品の洗浄方法 |
| JP4247587B2 (ja) | 1999-06-23 | 2009-04-02 | Jsr株式会社 | 半導体部品用洗浄剤、半導体部品の洗浄方法、研磨用組成物、および研磨方法 |
| JP4171858B2 (ja) | 1999-06-23 | 2008-10-29 | Jsr株式会社 | 研磨用組成物および研磨方法 |
| US6440856B1 (en) | 1999-09-14 | 2002-08-27 | Jsr Corporation | Cleaning agent for semiconductor parts and method for cleaning semiconductor parts |
| JP4273475B2 (ja) * | 1999-09-21 | 2009-06-03 | 株式会社フジミインコーポレーテッド | 研磨用組成物 |
| JP2001107089A (ja) | 1999-10-07 | 2001-04-17 | Jsr Corp | 半導体部品用洗浄剤、半導体部品の洗浄方法、研磨用組成物、および研磨方法 |
| US6348076B1 (en) | 1999-10-08 | 2002-02-19 | International Business Machines Corporation | Slurry for mechanical polishing (CMP) of metals and use thereof |
| US6638143B2 (en) | 1999-12-22 | 2003-10-28 | Applied Materials, Inc. | Ion exchange materials for chemical mechanical polishing |
| JP2001226666A (ja) | 2000-02-15 | 2001-08-21 | Hitachi Ltd | 研磨砥粒と研磨液及びその研磨方法並びに半導体装置の製造方法 |
| JP2001300285A (ja) | 2000-04-18 | 2001-10-30 | Sanyo Chem Ind Ltd | 研磨用砥粒分散剤及び研磨用スラリー |
| TWI281493B (en) | 2000-10-06 | 2007-05-21 | Mitsui Mining & Smelting Co | Polishing material |
| EP1369906B1 (en) | 2001-02-20 | 2012-06-27 | Hitachi Chemical Company, Ltd. | Polishing compound and method for polishing substrate |
| US6632259B2 (en) | 2001-05-18 | 2003-10-14 | Rodel Holdings, Inc. | Chemical mechanical polishing compositions and methods relating thereto |
| JP5017574B2 (ja) | 2001-05-25 | 2012-09-05 | エア プロダクツ アンド ケミカルズ インコーポレイテッド | 酸化セリウム研磨剤及び基板の製造方法 |
| JP4972829B2 (ja) | 2001-06-28 | 2012-07-11 | 日立化成工業株式会社 | Cmp研磨剤及び基板の研磨方法 |
| JP4076012B2 (ja) * | 2002-04-10 | 2008-04-16 | 株式会社日本触媒 | 化学機械研磨用水系分散体 |
| JP2003303792A (ja) * | 2002-04-10 | 2003-10-24 | Nippon Shokubai Co Ltd | 化学機械研磨用水系分散体と研磨方法 |
| JP2003313542A (ja) | 2002-04-22 | 2003-11-06 | Jsr Corp | 化学機械研磨用水系分散体 |
| JP2003347247A (ja) | 2002-05-28 | 2003-12-05 | Hitachi Chem Co Ltd | 半導体絶縁膜用cmp研磨剤及び基板の研磨方法 |
| KR100988749B1 (ko) * | 2002-07-22 | 2010-10-20 | 아사히 가라스 가부시키가이샤 | 반도체용 연마제, 그 제조 방법 및 연마 방법 |
| JP2004349426A (ja) * | 2003-05-21 | 2004-12-09 | Jsr Corp | Sti用化学機械研磨方法 |
| US20070218811A1 (en) * | 2004-09-27 | 2007-09-20 | Hitachi Chemical Co., Ltd. | Cmp polishing slurry and method of polishing substrate |
| US20080254717A1 (en) * | 2004-09-28 | 2008-10-16 | Hitachi Chemical Co., Ltd. | Cmp Polishing Slurry and Method of Polishing Substrate |
-
2005
- 2005-07-20 US US11/572,523 patent/US9293344B2/en active Active
- 2005-07-20 JP JP2006529234A patent/JPWO2006009160A1/ja active Pending
- 2005-07-20 CN CNA2005800235561A patent/CN1985361A/zh active Pending
- 2005-07-20 CN CN201110430594.6A patent/CN102585765B/zh not_active Expired - Lifetime
- 2005-07-20 CN CNA2008101292389A patent/CN101311205A/zh active Pending
- 2005-07-20 EP EP05766424.5A patent/EP1796152B1/en not_active Expired - Lifetime
- 2005-07-20 WO PCT/JP2005/013283 patent/WO2006009160A1/ja not_active Ceased
- 2005-07-20 KR KR1020077001589A patent/KR100856171B1/ko not_active Expired - Lifetime
- 2005-07-21 TW TW094124651A patent/TWI287040B/zh not_active IP Right Cessation
-
2011
- 2011-02-16 JP JP2011031168A patent/JP5509114B2/ja not_active Expired - Lifetime
-
2013
- 2013-03-04 JP JP2013042019A patent/JP5655879B2/ja not_active Expired - Lifetime
Non-Patent Citations (1)
| Title |
|---|
| None * |
Also Published As
| Publication number | Publication date |
|---|---|
| JP5655879B2 (ja) | 2015-01-21 |
| EP1796152A1 (en) | 2007-06-13 |
| TWI287040B (en) | 2007-09-21 |
| US20080003925A1 (en) | 2008-01-03 |
| JP2011103498A (ja) | 2011-05-26 |
| KR100856171B1 (ko) | 2008-09-03 |
| TW200609337A (en) | 2006-03-16 |
| US9293344B2 (en) | 2016-03-22 |
| EP1796152A4 (en) | 2008-12-03 |
| JPWO2006009160A1 (ja) | 2008-05-01 |
| CN102585765A (zh) | 2012-07-18 |
| CN1985361A (zh) | 2007-06-20 |
| CN101311205A (zh) | 2008-11-26 |
| JP5509114B2 (ja) | 2014-06-04 |
| JP2013149992A (ja) | 2013-08-01 |
| WO2006009160A1 (ja) | 2006-01-26 |
| CN102585765B (zh) | 2015-01-21 |
| KR20070026843A (ko) | 2007-03-08 |
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